US9644280B2 - Process for electrolytically depositing a tin- and ruthenium-based alloy, the electrolytic bath therefore and the alloy obtained therewith - Google Patents

Process for electrolytically depositing a tin- and ruthenium-based alloy, the electrolytic bath therefore and the alloy obtained therewith Download PDF

Info

Publication number
US9644280B2
US9644280B2 US14/759,293 US201314759293A US9644280B2 US 9644280 B2 US9644280 B2 US 9644280B2 US 201314759293 A US201314759293 A US 201314759293A US 9644280 B2 US9644280 B2 US 9644280B2
Authority
US
United States
Prior art keywords
electrolytic bath
salts
ruthenium
tin
group
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
US14/759,293
Other versions
US20150354076A1 (en
Inventor
Samuele BUSSETTI
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Valmet Plating SRL
Original Assignee
Valmet Plating SRL
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Valmet Plating SRL filed Critical Valmet Plating SRL
Assigned to VALMET PLATING SRL reassignment VALMET PLATING SRL ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: Bussetti, Samuele
Publication of US20150354076A1 publication Critical patent/US20150354076A1/en
Application granted granted Critical
Publication of US9644280B2 publication Critical patent/US9644280B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/56—Electroplating: Baths therefor from solutions of alloys
    • C25D3/60—Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of tin
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/56—Electroplating: Baths therefor from solutions of alloys

Definitions

  • the invention refers to the electrolytic deposition of a substantially tin- and ruthenium-based alloy having optimal features of corrosion resistance.
  • the invention refers to an ecologically compatible process to realize the electrolytic deposit of said alloy and to the operative conditions to realize said deposit.
  • the invention refers to the electrolytic bath by which said alloy is made to electro-deposit.
  • said electrolytic bath is advantageously distinguished by the total absence of toxic metals and cyanides.
  • the invention also refers to said alloy obtained through said process, as well as to the object/manufactured article covered with said alloy obtained through said process.
  • tin-based alloys are known.
  • those comprising also other metals such as, for example nickel, lead, copper, zinc, etc.
  • alkali electrolytic baths that contain cyanides are normally used. All this reflects negatively both from the point of view of toxicity of the baths and of their final products, and from the point of view of toxicity and/or of the eco-compatibility of the entire production process.
  • tin-based alloys known in the field which are deposited with a level of tin superior to the 50%, have, for example, a scarce resistance to fumes of nitric acid (as well as to acids in general), oxidizing and/or corroding too quickly.
  • alloys are not sufficiently resistant and contain, as additional components, or also just as traces, metals and/or residues of elaboration that are toxic for man and the environment.
  • It is another subject of the present invention is to provide the above mentioned electrolytic bath.
  • Another subject of the invention is also the substantially tin- and ruthenium-based alloy obtained through the above process.
  • It is another subject of the present invention is to provide an object/manufactured article realized through the electrolytic deposition method of the above described bath.
  • tin indifferently metal tin (Sn) and/or one or more salts thereof;
  • ruthenium it is intended indifferently metal ruthenium (Ru) and/or one or more salts thereof.
  • the present invention is directed to a process for electrolytically depositing a layer of a substantially tin- and ruthenium-based alloy on a cathode soaked into an aqueous electrolytic bath containing at least effective amounts of tin, ruthenium, conductor salts, complex-forming salts, alkali metal hydroxides, in which said process is characterized in that in said aqueous electrolytic bath:
  • tin under the form of metal or one or more of its salts
  • tin is present in an amount comprised between 1 and 100 g/L per liter of electrolytic bath; preferably, between 5 and 50 g/L; still more preferably, of about 15 g/L;
  • ruthenium (under the form of metal or one or more of its salts) is present in an amount comprised between 0.030 and 10 g/L per liter of electrolytic bath; preferably, between 0.1 and 5 g/L; still more preferably, of about 0.8 g/L;
  • the conductor salts taken alone or in a mixture thereof, are present in an overall amount comprised between 5 and 100 gr/L per liter of electrolytic bath; preferably, between 10 and 50 gr/L; still more preferably, of about 30 gr/L;
  • the complex forming salts are present in an overall amount comprised between 10 and 100 g/L per liter of electrolytic bath; preferably, between 20 and 50 gr/L; still more preferably, between 30 and 40 gr/L;
  • the alkali metal hydroxides are present in an amount comprised between 0.2 and 10 gr/lt per liter of electrolytic bath; preferably, between 1 and 3.5 g/L; still more preferably, of about 3 g/L;
  • tin salts according to the invention are preferably selected from tin (II) salts and tin (IV) salts;
  • examples of tin salts (II) comprise: sulphate, chloride, bromide, iodide, oxide, phosphate, pyrophosphate, acetate, citrate, gluconate, tartrate, lactate, succinate, sulphamate, phormiate;
  • tin (IV) salts comprise: sodium stannate, potassium stannate, nitrate, chloride and sulfide;
  • ruthenium salts according to the invention are preferably selected from ruthenium (III) salts and ruthenium (IV) salts;
  • ruthenium salts comprise the groups: sulfide, carboxylate, chlorides, bromides, oxalate, sulphamate, composed nitrile, oxydryl;
  • the conductor salts are preferably selected from the group consisting of: phosphates, carbonates, citrates, sulphates, tartrates, oxalates, sulphamates, gluconates, phosphonates, acetates and pyrophosphates;
  • the complex forming salts are preferably selected from the group consisting of: sulphates, carboxylates, chlorides, oxalates, pyrophosphates, citrates, sulphamates, gluconates, tartrates, phosphates, phosphonates;
  • the hydroxides of the alkali metals are selected from sodium hydroxide and potassium hydroxide.
  • the cathode is constituted, on the basis of the realization needs and of the applicative field, by an appropriate metal object/manufactured article, for example made of brass, zamak, iron or aluminium, preferably, previously covered with deposits of electrolytic copper, nickel, bronze, gold, palladium and the alloys thereof, and the like.
  • an appropriate metal object/manufactured article for example made of brass, zamak, iron or aluminium, preferably, previously covered with deposits of electrolytic copper, nickel, bronze, gold, palladium and the alloys thereof, and the like.
  • the anode or the anodes is/are generally made of titanium coated with platinum, ruthenium, iridium or alloys from these metals.
  • the process of electro-deposition of the present invention is made at pH values comprised between 10 and 14; preferably, between 11 and 13; still more preferably, of about 12.
  • the process of electro-deposition of the present invention is made at a temperature comprised between 30° C. and 75° C.; preferably, between 35° C. and 70° C. In a preferred embodiment of the invention, the temperature is comprised between 40° C. and 60° C.
  • the process of electro-deposit of the present invention is made at a density/intensity of current comprised between 0.5 and 5 Amp/dm 2 ; preferably, between 1 and 4 Amp/dm 2 .
  • the duration of the process of electro-deposition of the present invention is variable on the basis of the size of the object (the cathode) that wants to be coated with the tin-ruthenium alloy of the invention; of the intensity/density of the current employed; and of the thickness of the layer of alloy that is to be deposited.
  • the time of electro-deposition is on average variable between 1 and 10 min; preferably, between 2 and 6 min.
  • the electrolytic bath of the present invention can further comprise one or more additional components selected from the group consisting of wetting agents, depolarizing agents, rinse-aid/brightness giving agents, other metal traces, organometallic compounds, stabilizing agents.
  • the bath can comprise one or more among the following additional additives, possibly an appropriate mixture of them.
  • Said at least one wetting agent is selected from all those known that are compatible with alkali environments.
  • the wetting agent is selected from non-ionic surfactants.
  • non-ionic surfactants it is selected from the group consisting of: polyoxyethylene ⁇ -naphthol ether, polyoxyethylene alkyl ether, polyoxyethylene phenylether, polyoxyethylene alkylamino ether, polyethylene glycol.
  • the wetting agent can also be selected from one or more cationic surfactants, anionic surfactants or amphoteric surfactants.
  • Examples of cationic surfactants comprise: dodecyltrimethyl ammonium salt, hexadecyltrimethyl ammonium salt, octadecyltrimethyl ammonium salt, dodecyldimethyl ammonium salt, cetyltrimethyl ammonium salt, dodecyldimethyl ammonium betaine, octadecyldimethyl ammonium betaine, dimethylbenzyldodecyl ammonium salt, trimethylbenzyl ammonium salt, octacecylamino acetate and dodecilamino acetate.
  • anionic surfactants comprise: alkyl sulphates, sodium dodecyl sulphate, lauryl sulphate, lauryl sulphonate, dodecyl sulphate, octadecyl sulphate, polyoxyethylene alkylether sulphates, sodium polyoxyethylene (E012) nonyl ether sulphate, polyoxyethylene alkylphenylether sulphates, alkylbenzenesulphonates.
  • amphoteric surfactants comprise betaine and sulphobetaine.
  • a depolarizing agent preferably, da 1 a 10 g/L; still more preferably, of about 5 g/L.
  • said depolarizing agents are selected from the group consisting of: salts of alkali tartrates and alkali sulphites.
  • said rinse-aid/brightness giving agents are selected from the group consisting of: butyndiol derivatives, di-thiocarboxylic acids, rhodium salts, silver salts and saccharinates.
  • Modest amounts or traces in any case not superior to 5% in weight, with respect to the overall amount of the salts constituting the bath; preferably, not superior to 3%; of the following metals: Zn, Rh, Pd, Au, Ga, Bi, Ag, Ta, In, Fe.
  • the wetting agent can be indifferently any one of those described above, preferably the cetyltrimethylammonium chloride or the sodium dodecyl sulfate.
  • the wetting agent can be indifferently any one of those described before, preferably the cetyltrimethylammonium chloride or the sodium dodecyl sulfate.
  • the electrolytic bath is contained in a polypropylene bath (PVC) and can be thermo-regulated by means of a heater in quartz, PTFE, porcelain or steel.
  • PVC polypropylene bath
  • the electro-deposited alloy is provided with an optimal resistance to oxidation and to acid agents
  • the electro-deposited alloy is exempt from toxic and allergenic metals or metalloids
  • the electrolyte of the bath is totally exempt from cyanides and from other toxic and polluting substances;
  • the performance of the deposit process is at least equal, when not superior, to those of traditional processes
  • the layer deposited is provided with a good brightness and resistance to oxidation
  • the colour of the alloy is comprised between white and grey.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating And Plating Baths Therefor (AREA)

Abstract

The invention refers to the electrolytic deposit of a tin- and ruthenium-based alloy having good features of corrosion resistance. In particular, the invention refers to an ecologically compatible process to achieve the electrolytic deposit of the alloy and to the operative conditions to make the deposit. Moreover, the invention refers to the electrolytic bath from which the alloy is caused to electro-deposit. In particular, the electrolytic bath is advantageously distinguished by the total absence of toxic metals and cyanides. The invention refers also to the alloy obtained through that process, as well as to the object/manufactured article covered with the alloy obtained through that process.

Description

TECHNICAL FIELD
The invention refers to the electrolytic deposition of a substantially tin- and ruthenium-based alloy having optimal features of corrosion resistance. In particular, the invention refers to an ecologically compatible process to realize the electrolytic deposit of said alloy and to the operative conditions to realize said deposit.
Moreover, the invention refers to the electrolytic bath by which said alloy is made to electro-deposit. In particular, said electrolytic bath is advantageously distinguished by the total absence of toxic metals and cyanides.
The invention also refers to said alloy obtained through said process, as well as to the object/manufactured article covered with said alloy obtained through said process.
BACKGROUND ART
In the field of electro-deposition, for example in the decorative one, some types of tin-based alloys are known. Among the most commonly used there are those comprising also other metals such as, for example nickel, lead, copper, zinc, etc. This implies that, together with tin, also allergenic or toxic metals are currently co-deposited. Moreover, in order to obtain this result, alkali electrolytic baths that contain cyanides are normally used. All this reflects negatively both from the point of view of toxicity of the baths and of their final products, and from the point of view of toxicity and/or of the eco-compatibility of the entire production process.
Moreover, a great part of the tin-based alloys known in the field, which are deposited with a level of tin superior to the 50%, have, for example, a scarce resistance to fumes of nitric acid (as well as to acids in general), oxidizing and/or corroding too quickly.
To sum up what has been explained above, unfortunately said alloys are not sufficiently resistant and contain, as additional components, or also just as traces, metals and/or residues of elaboration that are toxic for man and the environment.
TECHNICAL PROBLEM
It remains desirable, among the operators of the field, the need to have at disposal a tin-based alloy which does not present the above cited inconveniences and that results also advantageous in terms of duration and of aesthetic aspect. Moreover, it is equally desirable that such an alloy can also be used as a re-enforcing under layer before the application of a final decorative finishing (said finishing is usually constituted by a thin layer of a precious metal), thus conferring further advantageous physical-chemical performances to the finite object.
It is the subject of the present invention to overcome all or at least a great part of these inconveniences, thus giving an adequate response to the above described technical problem.
DISCLOSURE OF INVENTION
The applicant has now totally unexpectedly found out that, by electrolytically depositing an appropriate substantially tin- and ruthenium-based alloy by an appropriate electrolytic bath (electrolyte) not containing toxic products and/or metals, it is possible to give an adequate response to the technical problem described before.
It is therefore the subject of the present invention a process to achieve the electrolytic (galvanic) deposition of a substantially tin- and ruthenium-based alloy on a cathode soaked into an appropriate electrolytic bath (electrolytic solution) containing at least an effective amount of tin, and/or of one of its salts, and at least an effective quantity of ruthenium, and/or of one of its salts.
It is another subject of the present invention is to provide the above mentioned electrolytic bath.
Another subject of the invention is also the substantially tin- and ruthenium-based alloy obtained through the above process.
It is another subject of the present invention is to provide an object/manufactured article realized through the electrolytic deposition method of the above described bath.
Further subjects of the present invention are also described hereinafter.
DETAILED DESCRIPTION OF THE INVENTION
Definitions:
from now onwards, for greater simplicity, by the term “tin” it is intended indifferently metal tin (Sn) and/or one or more salts thereof;
from now onwards, for greater simplicity, by the term “ruthenium” it is intended indifferently metal ruthenium (Ru) and/or one or more salts thereof.
The present invention is directed to a process for electrolytically depositing a layer of a substantially tin- and ruthenium-based alloy on a cathode soaked into an aqueous electrolytic bath containing at least effective amounts of tin, ruthenium, conductor salts, complex-forming salts, alkali metal hydroxides, in which said process is characterized in that in said aqueous electrolytic bath:
tin (under the form of metal or one or more of its salts) is present in an amount comprised between 1 and 100 g/L per liter of electrolytic bath; preferably, between 5 and 50 g/L; still more preferably, of about 15 g/L;
ruthenium (under the form of metal or one or more of its salts) is present in an amount comprised between 0.030 and 10 g/L per liter of electrolytic bath; preferably, between 0.1 and 5 g/L; still more preferably, of about 0.8 g/L;
the conductor salts, taken alone or in a mixture thereof, are present in an overall amount comprised between 5 and 100 gr/L per liter of electrolytic bath; preferably, between 10 and 50 gr/L; still more preferably, of about 30 gr/L;
the complex forming salts are present in an overall amount comprised between 10 and 100 g/L per liter of electrolytic bath; preferably, between 20 and 50 gr/L; still more preferably, between 30 and 40 gr/L;
the alkali metal hydroxides are present in an amount comprised between 0.2 and 10 gr/lt per liter of electrolytic bath; preferably, between 1 and 3.5 g/L; still more preferably, of about 3 g/L;
with the proviso that, in said electrolytic bath cyanides and toxic and allergenic metals or metalloids, such as Be, Ni, Cd, As, Tl, are absent.
In the method of the present invention:
the tin salts according to the invention are preferably selected from tin (II) salts and tin (IV) salts;
examples of tin salts (II) comprise: sulphate, chloride, bromide, iodide, oxide, phosphate, pyrophosphate, acetate, citrate, gluconate, tartrate, lactate, succinate, sulphamate, phormiate;
examples of tin (IV) salts comprise: sodium stannate, potassium stannate, nitrate, chloride and sulfide;
ruthenium salts according to the invention are preferably selected from ruthenium (III) salts and ruthenium (IV) salts;
examples of ruthenium salts comprise the groups: sulfide, carboxylate, chlorides, bromides, oxalate, sulphamate, composed nitrile, oxydryl;
the conductor salts are preferably selected from the group consisting of: phosphates, carbonates, citrates, sulphates, tartrates, oxalates, sulphamates, gluconates, phosphonates, acetates and pyrophosphates;
the complex forming salts are preferably selected from the group consisting of: sulphates, carboxylates, chlorides, oxalates, pyrophosphates, citrates, sulphamates, gluconates, tartrates, phosphates, phosphonates;
the hydroxides of the alkali metals are selected from sodium hydroxide and potassium hydroxide.
In the method of the present invention, the cathode is constituted, on the basis of the realization needs and of the applicative field, by an appropriate metal object/manufactured article, for example made of brass, zamak, iron or aluminium, preferably, previously covered with deposits of electrolytic copper, nickel, bronze, gold, palladium and the alloys thereof, and the like.
In the method of the present invention, the anode or the anodes is/are generally made of titanium coated with platinum, ruthenium, iridium or alloys from these metals.
The process of electro-deposition of the present invention is made at pH values comprised between 10 and 14; preferably, between 11 and 13; still more preferably, of about 12.
The process of electro-deposition of the present invention is made at a temperature comprised between 30° C. and 75° C.; preferably, between 35° C. and 70° C. In a preferred embodiment of the invention, the temperature is comprised between 40° C. and 60° C.
Moreover, the process of electro-deposit of the present invention is made at a density/intensity of current comprised between 0.5 and 5 Amp/dm2; preferably, between 1 and 4 Amp/dm2.
Moreover, during the realization of the method of the present invention, it is necessary to maintain constant a cathodic agitation and of the electrolyte.
The duration of the process of electro-deposition of the present invention is variable on the basis of the size of the object (the cathode) that wants to be coated with the tin-ruthenium alloy of the invention; of the intensity/density of the current employed; and of the thickness of the layer of alloy that is to be deposited. In any case, the time of electro-deposition is on average variable between 1 and 10 min; preferably, between 2 and 6 min.
The electrolytic bath of the present invention can further comprise one or more additional components selected from the group consisting of wetting agents, depolarizing agents, rinse-aid/brightness giving agents, other metal traces, organometallic compounds, stabilizing agents.
For example, in a preferred embodiment of the invention, the bath can comprise one or more among the following additional additives, possibly an appropriate mixture of them.
(i) Between 1 and 20 mL/L of at least a wetting agent; preferably between 2 and 10 mL/L; still more preferably, of about 5 mL/L.
Said at least one wetting agent is selected from all those known that are compatible with alkali environments.
Preferably, the wetting agent is selected from non-ionic surfactants. For example, it is selected from the group consisting of: polyoxyethylene β-naphthol ether, polyoxyethylene alkyl ether, polyoxyethylene phenylether, polyoxyethylene alkylamino ether, polyethylene glycol.
The wetting agent can also be selected from one or more cationic surfactants, anionic surfactants or amphoteric surfactants.
Examples of cationic surfactants comprise: dodecyltrimethyl ammonium salt, hexadecyltrimethyl ammonium salt, octadecyltrimethyl ammonium salt, dodecyldimethyl ammonium salt, cetyltrimethyl ammonium salt, dodecyldimethyl ammonium betaine, octadecyldimethyl ammonium betaine, dimethylbenzyldodecyl ammonium salt, trimethylbenzyl ammonium salt, octacecylamino acetate and dodecilamino acetate.
Examples of anionic surfactants comprise: alkyl sulphates, sodium dodecyl sulphate, lauryl sulphate, lauryl sulphonate, dodecyl sulphate, octadecyl sulphate, polyoxyethylene alkylether sulphates, sodium polyoxyethylene (E012) nonyl ether sulphate, polyoxyethylene alkylphenylether sulphates, alkylbenzenesulphonates.
Examples of amphoteric surfactants comprise betaine and sulphobetaine.
(ii) Between 0.1 and 20 g/L of a depolarizing agent; preferably, da 1 a 10 g/L; still more preferably, of about 5 g/L.
Preferably, said depolarizing agents are selected from the group consisting of: salts of alkali tartrates and alkali sulphites.
(iii) Between 0.010 and 5 mL/L of at least a rinse-aid/brightness giving agent; preferably between 0.050 and 3 mL/L; still more preferably, of about 0,100 mL/L.
Preferably, said rinse-aid/brightness giving agents are selected from the group consisting of: butyndiol derivatives, di-thiocarboxylic acids, rhodium salts, silver salts and saccharinates.
(iv) Modest amounts or traces, in any case not superior to 5% in weight, with respect to the overall amount of the salts constituting the bath; preferably, not superior to 3%; of the following metals: Zn, Rh, Pd, Au, Ga, Bi, Ag, Ta, In, Fe.
The examples that follow have the only purpose of illustrating the invention in detail, in particular, the composition of the electrolytic bath from which it is possible to obtain/deposit the alloy that is the subject of the present invention and are absolutely not limiting of the wide applicative potential of the same.
EXAMPLE 1
Composition of an aqueous electrolytic bath according to the invention and its application:
Sn 15 g/L
Ru 0.8 g/L 
KOH  4 g/L
Wetting agent 0.01 g/L 
Potassium oxalate  5 g/L
Potassium citrate 30 g/L
In the present example, the wetting agent can be indifferently any one of those described above, preferably the cetyltrimethylammonium chloride or the sodium dodecyl sulfate.
In the present example the pH of the bath is =12; the operating temperature is =50° C. and the density of current employed is =2 Amp·dm2.
EXAMPLE 2
Composition of an aqueous electrolytic bath according to the invention and its application:
Sn 25 g/L
Ru 0.9 g/L 
KOH  4 g/L
Wetting agent 0.01 g/L 
Potassium oxalate  2 g/L
Sodium and potassium tartrate 50 g/L
In the present example, the wetting agent can be indifferently any one of those described before, preferably the cetyltrimethylammonium chloride or the sodium dodecyl sulfate.
In the present example the pH of the bath is =12; the operating temperature is =45° C. and the density of current employed is =1 Amp·dm2.
Moreover, in the present example the electrolytic bath is contained in a polypropylene bath (PVC) and can be thermo-regulated by means of a heater in quartz, PTFE, porcelain or steel.
The present invention is not limited by the examples illustrated; many variants and alternatives are in fact possible that will result easily realizable by the experts in the field in the light of the teaching of the present description and of the attached claims.
Some of the advantageous features of the present invention are represented, among others, by the following aspects:
the electro-deposited alloy is provided with an optimal resistance to oxidation and to acid agents;
the electro-deposited alloy is exempt from toxic and allergenic metals or metalloids;
the electrolyte of the bath is totally exempt from cyanides and from other toxic and polluting substances;
the performance of the deposit process is at least equal, when not superior, to those of traditional processes;
the layer deposited is provided with a good brightness and resistance to oxidation;
great homogeneity of the distribution of the alloy to the different densities of current has been found also on cathodes of complex shapes and not linear;
the colour of the alloy is comprised between white and grey.
The advantages obtained with the method of the present invention derive in particular also from the type of electrolytic bath employed.
As a consequence, also said bath, as described in the preceding description, is one of the subjects of the present invention.
Substantially tin- and ruthenium-based alloys, deposited electrolytically on an object (cathode) in accordance with the method of the present invention, are not known until now to the best of knowledge of the applicant.
As a consequence, also said Sn—Ru alloy, as described in the preceding description, is one of the subjects of the present invention.
In the light of all the above, it is a further subject of the present invention also a manufactured product/an article coated with said Sn—Ru alloy realized through the method of electrolytic deposit from the electrolytic bath of the present invention.
It is also a further subject of the present invention a substantially tin- and ruthenium-based alloy obtained with the process as described herein.
It is also a further subject of the present invention an article/manufactured article coated with a substantially tin- and ruthenium-based alloy obtained as described above.

Claims (16)

The invention claimed is:
1. A process for electrolytically depositing a layer of a tin- and ruthenium-based alloy on a cathode soaked into an aqueous electrolytic bath, comprising:
providing, in said aqueous electrolytic bath, at least:
tin in an amount comprised between 1 and 100 g/L of electrolytic bath;
ruthenium in an amount comprised between 0.030 and 10 g/L of electrolytic bath;
one or more conductor salts in an amount comprised between 5 and 100 g/L of electrolytic bath;
complex forming salts in an amount comprised between 10 and 100 g/L of electrolytic bath; and
alkali metal hydroxides in an amount comprised between 0.2 and 10 g/L of electrolytic bath;
wherein, in said electrolytic bath,
cyanides,
toxic and allergenic metals or metalloids, and
Be, Ni, Cd, As, and Tl
are absent; and
electrolytically depositing the layer of the tin- and ruthenium based alloy on the cathode soaked in the aqueous electrolytic bath.
2. The process according to claim 1, wherein:
tin is selected from the group consisting of metallic tin, tin (II) salts, and tin (IV) salts;
ruthenium is selected from the group consisting of metallic ruthenium, ruthenium (III) salts, and ruthenium (IV) salts;
the conductor salts are selected from the group consisting of phosphates, carbonates, citrates, sulphates, tartrates, oxalates, sulphamates, gluconates, phosphonates, acetates, and pyrophosphates; and
the alkali metal hydroxides are selected from the group consisting of sodium hydroxide and potassium hydroxide.
3. The process according to claim 1, wherein:
the cathode is made of metal, brass, zamak, plastic, ABS (Acrylonitrile Butadiene Styrene), iron or aluminum; and
one or more anodes are made of titanium coated with platinum, ruthenium, graphite, iridium, or alloys thereof.
4. The process according to claim 1, wherein: pH is comprised between 10 and 14;
temperature is comprised between 30° C. and 75° C.; and
current intensity is comprised between 0.5 and 5 Amp/dm2.
5. The process according to claim 1, wherein said electrolytic bath further comprises one or more additional components selected from the group consisting of wetting agents, depolarizing agents, rinse-aid/brightness giving agents, other metals in traces, organometallic compounds, stabilizing agents, and mixture thereof.
6. The process according to claim 5, wherein said wetting agents are present in a total amount comprised between 1 and 20 mL/L and are selected from the group consisting of:
non-ionic surfactants including one or more of polyoxyethylene β-naphthol ether, polyoxyethylene alkyl ether, polyoxyethylene phenylether, polyoxyethylene alkylamino ether, or polyethylene glycol;
cationic surfactants including one or more of dodecyltrimethyl ammonium salt, hexadecyltrimethyl ammonium salt, octadecyltrimethyl ammonium salt, dodecyldimethyl ammonium salt, cetyltrimethyl ammonium salt, dodecyldimethyl ammonium betaine, octadecyldimethyl ammonium betaine, dimethylbenzyldodecyl ammonium salt, trimethylbenzyl ammonium salt, octacecylamino acetate, or dodecilamino acetate;
anionic surfactants including one or more of alkyl sulphates, sodium dodecyl sulphate, lauryl sulphate, lauryl sulphonate, dodecyl sulphate, octadecyl sulphate, polyoxyethylene alkylether sulphates, sodium polyoxyethylene (EO12) nonyl ether sulphate, polyoxyethylene alkylphenylether sulphates, or alkylbenzenesulphonates; and
amphoteric surfactants including one or more of betaine or sulphobetaine.
7. The process according to claim 5, wherein said depolarizing agents are present in a total amount comprised between 0.1 and 20 g/L, and are selected from the group consisting of: salts of alkali tartrates and alkali sulphites.
8. The process according to claim 5, wherein said rinse-aid/brightness giving agents are present in a total amount comprised between 0.010 and 5 mL/L, and are selected from the group consisting of: butyndiol derivatives, di-thiocarboxylic acids, rhodium salts, silver salts, and saccharinates.
9. The process according to claim 5, wherein said other metals are present in an amount not higher than 5%, with reference to a total amount of salts in the electrolytic bath, and are selected from the group consisting of: Zn, Rh, Pd, Au, Ga, Bi, Ag, Ta, In, and Fe.
10. An electrolytic bath for depositing a layer of a tin- and ruthenium-based alloy on a cathode, comprising:
tin in an amount comprised between 1 and 100 g/L of electrolytic bath;
ruthenium in an amount comprised between 0.030 and 10 g/L of electrolytic bath;
one or more conductor salts in an amount comprised between 5 and 100 g/L of electrolytic bath;
complex forming salts in an amount comprised between 10 and 100 g/L of electrolytic bath; and
alkali metal hydroxides in an amount comprised between 0.2 and 10 g/L of electrolytic bath;
wherein, in said electrolytic bath,
cyanides, and
toxic and allergenic metals or metalloids, and
Be, Ni, Cd, As, and Tl
are absent.
11. The electrolytic bath according to claim 10, wherein:
tin is selected from the group consisting of metallic tin, tin (II) salts, and tin (IV) salts;
ruthenium is selected from the group consisting of metallic ruthenium, ruthenium (III) salts, and ruthenium (IV) salts;
the conductor salts are selected from the group consisting of phosphates, carbonates, citrates, sulphates, tartrates, oxalates, sulphamates, gluconates, phosphonates, acetates, and pyrophosphates; and
the alkali metal hydroxides are selected from the group consisting of sodium hydroxide and potassium hydroxide.
12. The electrolytic bath according to claim 10, wherein:
pH is comprised between 10 and 14;
temperature is comprised between 30° C. and 75° C.; and
current intensity is comprised between 0.5 and 5 Amp/dm2,
further comprising one or more additional components selected from the group consisting of wetting agents, depolarizing agents, rinse-aid/brightness giving agents, other metals in traces, organometallic compounds, stabilizing agents, and mixture thereof.
13. The electrolytic bath according to claim 12, wherein said wetting agents are present in a total amount comprised between 1 and 20 mL/L and are selected from the group consisting of:
non-ionic surfactants including one or more of polyoxyethylene β-naphthol ether, polyoxyethylene alkyl ether, polyoxyethylene phenylether, polyoxyethylene alkylamino ether, or polyethylene glycol;
cationic surfactants including one or more of dodecyltrimethyl ammonium salt, hexadecyltrimethyl ammonium salt, octadecyltrimethyl ammonium salt, dodecyldimethyl ammonium salt, cetyltrimethyl ammonium salt, dodecyldimethyl ammonium betaine, octadecyldimethyl ammonium betaine, dimethylbenzyldodecyl ammonium salt, trimethylbenzyl ammonium salt, octacecylamino acetate, or dodecilamino acetate;
anionic surfactants including one or more of alkyl sulphates, sodium dodecyl sulphate, lauryl sulphate, lauryl sulphonate, dodecyl sulphate, octadecyl sulphate, polyoxyethylene alkylether sulphates, sodium polyoxyethylene (EO12) nonyl ether sulphate, polyoxyethylene alkylphenylether sulphates, or alkylbenzenesulphonates; and
amphoteric surfactants including one or more of betaine or sulphobetaine.
14. The electrolytic bath according to claim 12, wherein said depolarizing agents are present in a total amount comprised between 0.1 and 20 g/L, and are selected from the group consisting of: salts of alkali tartrates and alkali sulphites.
15. The electrolytic bath according to claim 12, wherein said rinse-aid/brightness giving agents are present in a total amount comprised between 0.010 and 5 mL/L, and are selected from the group consisting of: butyndiol derivatives, di-thiocarboxylic acids, rhodium salts, silver salts, and saccharinates.
16. The electrolytic bath according to claim 12, wherein said other metals are present in an amount not higher than 5%, with reference to a total amount of salts in the electrolytic bath, and are selected from the group consisting of: Zn, Rh, Pd, Au, Ga, Bi, Ag, Ta, In, and Fe.
US14/759,293 2013-01-18 2013-11-18 Process for electrolytically depositing a tin- and ruthenium-based alloy, the electrolytic bath therefore and the alloy obtained therewith Active US9644280B2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
EP13425013.3A EP2757180B1 (en) 2013-01-18 2013-01-18 A process for electrolytically depositing a tin- and ruthenium-based alloy, the electrolytic bath that permits said alloy to deposit and the alloy obtained by means of said process
EP13425013.3 2013-01-18
EP13425013 2013-01-18
PCT/IB2013/060214 WO2014111761A1 (en) 2013-01-18 2013-11-18 A process for electrolytically depositing a tin- and ruthenium-based alloy, the electrolytic bath that permits said alloy to deposit and the alloy obtained by means of said process

Publications (2)

Publication Number Publication Date
US20150354076A1 US20150354076A1 (en) 2015-12-10
US9644280B2 true US9644280B2 (en) 2017-05-09

Family

ID=48182872

Family Applications (1)

Application Number Title Priority Date Filing Date
US14/759,293 Active US9644280B2 (en) 2013-01-18 2013-11-18 Process for electrolytically depositing a tin- and ruthenium-based alloy, the electrolytic bath therefore and the alloy obtained therewith

Country Status (3)

Country Link
US (1) US9644280B2 (en)
EP (1) EP2757180B1 (en)
WO (1) WO2014111761A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3150744B1 (en) 2015-09-30 2020-02-12 COVENTYA S.p.A. Electroplating bath for electrochemical deposition of a cu-sn-zn-pd alloy layer, method for electrochemical deposition of said alloy layer, substrate comprising said alloy layer and uses of the coated substrate
WO2021199087A1 (en) * 2020-03-30 2021-10-07 Italfimet Srl Galvanic process for the electrodeposition of a protective layer, and associated bath
AT523922B1 (en) * 2020-09-08 2022-01-15 Iwg Ing W Garhoefer Ges M B H Electrolyte bath for palladium-ruthenium coatings
DE102020131371B4 (en) * 2020-11-26 2024-08-08 Umicore Galvanotechnik Gmbh Use of an electrolyte to produce a ruthenium alloy layer
CN115261937A (en) * 2022-03-22 2022-11-01 东莞市弘裕表面处理技术有限公司 Ruthenium plating solution, method for preparing ruthenium plating solution, ruthenium plating method, ruthenium plating layer, and device containing ruthenium plating layer

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3933602A (en) * 1973-04-27 1976-01-20 Oxy Metal Industries Corporation Palladium electroplating bath, process, and preparation
US4686017A (en) * 1981-11-05 1987-08-11 Union Oil Co. Of California Electrolytic bath and methods of use
US4749626A (en) 1985-08-05 1988-06-07 Olin Corporation Whisker resistant tin coatings and baths and methods for making such coatings
US6361823B1 (en) 1999-12-03 2002-03-26 Atotech Deutschland Gmbh Process for whisker-free aqueous electroless tin plating
US20050173255A1 (en) * 2004-02-05 2005-08-11 George Bokisa Electroplated quaternary alloys

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3933602A (en) * 1973-04-27 1976-01-20 Oxy Metal Industries Corporation Palladium electroplating bath, process, and preparation
US4686017A (en) * 1981-11-05 1987-08-11 Union Oil Co. Of California Electrolytic bath and methods of use
US4749626A (en) 1985-08-05 1988-06-07 Olin Corporation Whisker resistant tin coatings and baths and methods for making such coatings
US6361823B1 (en) 1999-12-03 2002-03-26 Atotech Deutschland Gmbh Process for whisker-free aqueous electroless tin plating
US20050173255A1 (en) * 2004-02-05 2005-08-11 George Bokisa Electroplated quaternary alloys

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
Dos Santos S M et al: "Performance of RuSn catalysts supported on different oxides in the selective hydrogenation of dimethyl adipate," CATALYSIS TODAY, Elsevier, NL, vol. 107-108, Oct. 30, 2005, pp. 250-257 p. 251, right-hand column, para. 2; Experimental.
Springerova Jana et al: "Selective hydrogenation of .alpha., .beta.-unsaturated carbonyl compounds on supported Ru-Sn catalysts," Research of Chemical Intermediates, Amsterdam, NL, vol. 31, No. 9, Jan. 1, 2005, pp. 785-795 Abstract; pp. 786-787, paragraph materials and methods; p. 790; Table 1.
Springerova Jana et al: "Selective hydrogenation of .alpha., .beta.-unsaturated carbonyl compounds on supported Ru—Sn catalysts," Research of Chemical Intermediates, Amsterdam, NL, vol. 31, No. 9, Jan. 1, 2005, pp. 785-795 Abstract; pp. 786-787, paragraph materials and methods; p. 790; Table 1.

Also Published As

Publication number Publication date
EP2757180B1 (en) 2015-08-12
WO2014111761A1 (en) 2014-07-24
EP2757180A1 (en) 2014-07-23
US20150354076A1 (en) 2015-12-10

Similar Documents

Publication Publication Date Title
US9644280B2 (en) Process for electrolytically depositing a tin- and ruthenium-based alloy, the electrolytic bath therefore and the alloy obtained therewith
JP2011520037A (en) Improved copper-tin electrolyte and bronze layer deposition method
JP2014519555A (en) Electrolyte, its use for the deposition of black ruthenium coating and the coating so obtained
JP2014194087A (en) Method for obtaining yellow gold alloy deposits based on an electroplating method without using toxic metals or metalloids
EP3067444B1 (en) Deposition of decorative palladium iron alloy coatings on metallic substances
GB1239862A (en) Tin-nickel plated copper articles and process of manufacture
JP5563421B2 (en) Method for obtaining yellow gold alloy deposits by electroplating without using toxic metals
US3206382A (en) Electrodeposition of platinum or palladium
US4297179A (en) Palladium electroplating bath and process
US4566953A (en) Pulse plating of nickel-antimony films
JPH1060683A (en) Electroplating with ternary system zinc alloy, and its method
DE102020131371B4 (en) Use of an electrolyte to produce a ruthenium alloy layer
JP4517177B2 (en) Treatment method of electroless nickel plating solution
JP3277816B2 (en) Ternary zinc alloy electroplating method
JP6969688B2 (en) Electroplating bath, manufacturing method of electroplating products, and electroplating equipment
US3890210A (en) Method and electrolyte for electroplating rhodium-rhenium alloys
US20240150920A1 (en) Platinum Electrolyte
GB760084A (en) Improvements in and relating to the electrodeposition of antimony
US2057475A (en) Electrodeposition of rhodium
JP6116980B2 (en) Al substrate with Mn layer
CN117265607A (en) Blind hole metal piece and electroplating method thereof
JPS6070197A (en) Silver alloy plating method
GB525364A (en) Improved process and apparatus for the electro-deposition of tin alloys
JPS6312954B2 (en)
Subramaniyan Electrodeposition of copper-lead alloys from a methanesulfonic acid electrolyte/Balachandar a/l Subramaniyan

Legal Events

Date Code Title Description
AS Assignment

Owner name: VALMET PLATING SRL, ITALY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:BUSSETTI, SAMUELE;REEL/FRAME:035982/0119

Effective date: 20150701

STCF Information on status: patent grant

Free format text: PATENTED CASE

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 4TH YR, SMALL ENTITY (ORIGINAL EVENT CODE: M2551); ENTITY STATUS OF PATENT OWNER: SMALL ENTITY

Year of fee payment: 4

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 8TH YR, SMALL ENTITY (ORIGINAL EVENT CODE: M2552); ENTITY STATUS OF PATENT OWNER: SMALL ENTITY

Year of fee payment: 8